US3053637A

US3053637A - Production of pure phosphorus

Info

Publication number: US3053637A
Application number: US860666A
Authority: US
Inventors: Forrest V Williams
Original assignee: Monsanto Chemicals Ltd
Current assignee: Monsanto Chemicals Ltd; Monsanto Chemical Co
Priority date: 1959-12-21
Filing date: 1959-12-21
Publication date: 1962-09-11
Anticipated expiration: 1979-09-11

Description

United States Patent 3,053,637 PRODUCTION OF PURE PHOSPHORUS Forrest V. Williams, Dayton, Ohio, assignor to Monsanto Chemical Company, St. Louis, Mo., a corporation of Delaware No Drawing. Filed Dec. 21, 1959, Ser. No. 860,666 6 Claims. (Cl. 23223) The present invention relates to the production of very pure phosphorus suitable for use in the manufacture of electronic and semiconductor materials such as indium phosphide, gallium phosphide, aluminum phosphide, baron phosphide, zinc phosphide, and mixed metal phosphides.

It is an object of the invention to prepare phosphorus in a form which is relatively free from impurities and which is more uniform in its electrical characteristics as well as in its chemical derivatives than has been possible by prior art methods.

In the production of elemental phosphorus, it has been found that the chemical elements which occur together with the phosphorus are carried into the product. Examples of such impurities include the halogen elements such as fluorine, chlorine, etc., and also sulfur compounds. Certain forms of phosphorus such as the so-called white phosphorus which are stored under water or oil may also pick up impurities therefrom. It has been attempted to purify the elemental phosphorus by distillation, but the conventional distillation processes have been found to offer little improvement in the purity of the phosphorus which is thus obtained.

It has now been found that elemental forms of phosphorus including both the white and red forms may be greatly improved in purity by treatment of the phosphorus at a specific range of elevated temperatures in the pres ence of a treating agent selected from the class consisting of argon and helium gases. In order to carry out such a purification, the phosphorus may be passed directly into a heated conduit made of an inert material such as quartz, while at the same time introducing argon or helium gas or mixtures of argon and helium in any proportions, and subjecting the mixture of the gaseous phosphorus and the argon and/or helium gases to the said high temperatu-re.

It has been found that a temperature in the range of from 850 C. to l,0O0 C. is of utility for this purpose, a preferred range being from 900 C. to 950 C. It is preferred that the treatment with the gas such as argon be conducted in the substantial absence of any other gases. Reactive gases, such as oxygen, even in minor traces, must be rigorously excluded from the reaction system. The time during which the phosphorus is in contact with the argon or helium is not critical and may be varied as convenient from a minute or less to an hour or more. The pressure is likewise a non-critical variable, so that vacuum, atmospheric and pressure conditions maybe used as desired.

The proportion of argon or helium which is employed in the present treating method is not critical. It has been found that the present process is applicable, both with the use of very small proportions, i.e., 0.01 mole of phosphorus as well as large excesses, e.g., 100 moles of argon or helium per mole of phosphorus are all effective in carrying out the present purification method. The argon or helium used may be of conventional commercial purity, or may be purified by chemical means.

After the phosphorus has been contacted with the helium or argon in vapor phase, such as by passing the gaseous mixture through a packed section of a conduit, e.g., by passage through quartz beads or quartz wool located in a quartz tube at the said elevated temperature, the phosphorus is collected by conventional means. In the method described, using a continuous conduit, the collection zone may be a cooler section of the tubular reactor or a cool condenser. If desired, receiving vessels which may be sealed off may also be employed in this purpose, thereby permitting the phosphorus to be collected in an end tube provided with a gas vent. The collection tube is thereafter sealed off to keep the phosphorus free from contact with air and other impurities until it is desired for further use.

In the manufacture of electronic and semiconductor components, it has been found that phosphorus compounds must be of an unusually high order of purity in order to function uniformly and effectively in these fields. For example, in the manufacture of indium phosphide, a sample of the purified phosphorus collected in a sealed oif tube as described above, may later by connected to a gaseous reaction system. The phosphorus is then heated in its tube in order to volatilize the said phosphorus into a further tubular section in which elemental indium is located. The phosphorus then reacts with the indium to give the desired indium phosphide. By such methods, other semiconductor components, such as gallium phosphide, alluminum phosphide, boron phosphide, and zinc phosphide, may also be prepared. Mixed metal phosphides such as zinc germanium phosphide, ZnGeP are also readily prepared from the present purified form of elemental phosphorus prepared in accordance with the method of the present invention.

The apparatus employed in carrying out the present invention may also be modified to use vertical tubes, for example, in which phosphorus is volatilized from either the white or red form maintained in a storage receptacle, directly into a tubular section where it is contacted with argon or helium at the aforesaid higher temperature, and then condensed in a suitable vessel. However, it has been found that the temperature range of from 850 to 1000 C. is critical in this relationship, and that the use of a lower temperature such as 700 C. does not effect any purification. It has also been found that the more sublimation of elemental phosphorus in a vacuum, for example, at 450 C. which is a conventional sublimation temperature, does not accomplish the purification which is achieved by the practice of the present invention.

The following examples illustrate specificembodiments of the present invention.

Example 1 The purification of red phosphorus was carried out by placing a quartz boat of phosphorus in a quartz tube of one inch diameter and 24 inch length. The quartz tube was provided with two independent heating jackets as well as a third cooling section located in the atmosphere. At the inlet end of the tube, a connection was provided for the introduction of gaseous argon in the tube, while at the exit end a vacuum connection was provided as well as a previously prepared seal-off section for the collection of the purified phosphorus in a sealed-oft quartz tube. The first furnace which was placed around the tube and the boat containing the red phosphorus was heated to a temperature of 450 C. while the middle reactor section which was packed with quartz beads located in the quartz tube, was maintained at a temperature of 925 C. The third section was at 200 C., with the cool end at substantially atmospheric temperature. A stream of argon at the rate of 50-60 cc. per minute was introduced into the tube, thereby volatilizing phosphorus from the supply of 18.61 grams of red phosphor-us. This gaseous mixture of argon and phosphorus, in the substantial absence of any other gases was then passed into the reactor section. The gaseous mixture after the purification had been completed, passed to the condenser section where the phosphorus condensed' on the walls of the quartz receiving tube, while the argon was withdrawn from the system. The pressure in the reaction system was maintained at 760 mm. Hg. After the above process had been conducted for a period of 2 hours, the receiving tube was sealed off, subjected to vacuum, and the vacuum connection sealed off to yield the purified phosphorus in an evacuated tube for storage until needed for subsequent processing.

Example 2 A similar test as described above but with the use of white phosphorus was also found to give a purified product.

Example 3 A similar test as described above in Example 1, but with 50-60 cc. per minute of helium in treating red phosphorus was found to give a purified product. However, a control test showed that if the phosphorus is distilled at 450 C. without the helium or argon, the product is of a lower purity.

The great purity of the phosphorus produced in accordance with the method of the present invention is difficult to analyze by conventional chemical methods, and it was therefore found that an adequate indication of purity could only be obtained by utilizing the purified phosphorus for reaction with indium in order to make indium phosphide, and then to determine the electronic properties of such indium phosphide. The indium phosphide thus prepared by volatilizing the phosphorus into a body of metallic indium (99.999% employing a temperature of 450 C. to volatilize the phosphorus, and a temperature of 1060 C. to effect the reaction of the indium and the phosphorus, gave a crystalline form of indium phosphide. This product was subjected to measurement of the electrical properties to determine the concentration of impurities expressed as atoms of impurities per cc. of indium phosphide.

The electrical properties (impurity concentration as atoms/cc.) for the varous test samples are summarized below:

Impurity Conc., Atoms/cc. of InP Reagent Conditions 715 C. (No argon). 3. 5X10 215 C. (No argon) 5. 5X10" 925 C. argon 4.2)(

11. Process for the purification of elemental phosphorus having fluorine, chlorine and sulfur compounds present.

therein as impurities which comprises volatilizing the phosphorus to the gas phase, with a treating agent selected from the group consisting of argon and helium, and contacting the said mixture at a temperature in the range of from 850 C. to 1000 C., and thereafter cooling the said gaseous mixture to condense the purified phosphorus.

2. Process for the purification of elemental phosphorus having fluorine, chlorine and sulfur compounds present therein as impurities which comprises volatilizing the phosphorus to the gas phase, with argon, and contacting the said mixture at a temperature in the range of from 850 C. to 1000 C., and thereafter cooling the said gaseous mixture to condense the purified phosphorus.

3. Process for the purification of elemental phosphorus having fluorine, chlorine and sulfur compounds present therein as impurities which comprises volatilizing the phosphorus to the gas phase, with helium, and contacting the said mixture at a temperature in the range of from 850 C. to 1000 C, and thereafter cooling the said gaseous mixture to condense the purified phosphorus.

4. Process for the purification of elemental phosphorus having fluorine, chlorine and sulfur compounds present therein as impurities which comprises volatilizing the phosphorus to the gas phase, and contacting the same with gaseous argon in the substantial absence of other gases at a temperature in the range of 900 C. to 950 C., and thereafter cooling the said gaseous mixture to condense the purified phosphorus.

5. Process for the purification of elemental phosphorus having fluorine, chlorine and sulfur compounds present therein as impurities which comprises volatilizing the phosphorus to the gas phase, with gaseous argon and contacting the said mixture at a temperature in the range of from 900 C. to 950 C., and thereafter cooling the said gaseous mixture to condense the purified phosphorus.

6. Process for the purification of elemental phosphorus having fluorine, chlorine and sulfur compound present therein as impurities which comprises volatilizing the phosphorus to the gas phase, with gaseous argon in the substantial absence of other gases and contacting the said mixture at a temperature in the range of from 900 C. to 950 C., and thereafter cooling the said gaseous mixture to condense the purified phosphorus.

and Theoretical Chemistry, vol. 8, pp. 742, 743 and 783, Longmans, Green and (30., NY.

Claims

1. PROCESS THE PURIFICATION OF ELEMENTAL PHOSPHORUS HAVING FLUORINE, CHLORINE AND SULFUR COMPOUNDS PRESENT THEREIN AS IMPURITIES WHICH COMPRISES VOLATILIZING THE PHOSPHORUS TO THE GAS PHASE, WITH A TREATING AGENT SELECTED FROM THE GOUP CONSISTING OF ARGON AND HELIUM, AND CONTACTING THE SAID MIXTURE AT A TEMPERATURE IN THE RANGE OF FROM 850* C. TO 1000* C., AND THEREAFTER COOLING THE SAID GASEOUS MIXTURE TO CONDENSE THE PURIFIED PHOSPHORUS.